Hydrotreatment and catalytic cracking combined processing method of residual oil
A catalytic cracking and combined processing technology, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, can solve the problems of underutilization of substances and reduction of catalyst activity, etc., achieve high conversion rate, increase hydrogen content, increase conversion rate effect
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Embodiment 1
[0019] A combined processing method of residual oil hydrotreating and catalytic cracking in this embodiment comprises the following steps:
[0020] (1) Under the presence of hydrogen and hydrogenation catalyst, carry out hydrogenation reaction in the hydrotreating unit with residual oil, catalytic cracking heavy diesel oil, and optional oil slurry distillate, the hydrogen partial pressure is 10MPa, and the temperature is 350 °C, the volume ratio of hydrogen to the material to be hydrogenated is 1000:1, and the volumetric space velocity of the material to be hydrogenated is 0.5h -1 , to obtain gas, naphtha, hydrogenated diesel oil and oil slurry distillate;
[0021] (2) After steaming out gasoline and diesel oil, utilize maleic anhydride-acrylamide-methacrylic acid copolymer demetallization agent to carry out demetallization treatment to liquid phase stream and carry out pretreatment to liquid phase stream, reduce metal content;
[0022] (3) Under catalytic cracking conditions...
Embodiment 2
[0025] A combined processing method of residual oil hydrotreating and catalytic cracking in this embodiment comprises the following steps:
[0026] (1) Residual oil, catalytic cracking heavy diesel oil, optional oil slurry distillate, in the presence of hydrogen and hydrogenation catalyst, carry out hydrogenation reaction in a hydrotreating unit, the hydrogen partial pressure is 8MPa, and the temperature is 350 -370°C, the volume ratio of hydrogen to the material to be hydrogenated is 800:1, and the volumetric space velocity of the material to be hydrogenated is 1.2h -1 , to obtain gas, naphtha, hydrogenated diesel oil and oil slurry distillate;
[0027] (2) After steaming out gasoline and diesel oil, utilize maleic anhydride-acrylamide-methacrylic acid copolymer demetallization agent to carry out demetallization treatment to liquid phase stream and carry out pretreatment to liquid phase stream, reduce metal content;
[0028] (3) Under catalytic cracking conditions, the pretr...
Embodiment 3
[0031] A combined processing method of residual oil hydrotreating and catalytic cracking in this embodiment comprises the following steps:
[0032] (1) Residual oil, catalytic cracking heavy diesel oil, optional oil slurry distillate, in the presence of hydrogen and hydrogenation catalyst, carry out hydrogenation reaction in the hydrotreating unit, the hydrogen partial pressure is 12MPa, and the temperature is 380 -400°C, the volume ratio of hydrogen to the material to be hydrogenated is 1200:1, and the volumetric space velocity of the material to be hydrogenated is 1.8h -1 , to obtain gas, naphtha, hydrogenated diesel oil and oil slurry distillate;
[0033] (2) After steaming out gasoline and diesel oil, utilize maleic anhydride-acrylamide-methacrylic acid copolymer demetallization agent to carry out demetallization treatment to liquid phase stream and carry out pretreatment to liquid phase stream, reduce metal content;
[0034] (3) Under catalytic cracking conditions, the p...
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